JPS59104348A - Spherical or semispherical tetrakis (3-(3,5-di-tert-butyl-4- hydroxyphenyl)propionyloxymethyl)methane and preparation thereof - Google Patents

Spherical or semispherical tetrakis (3-(3,5-di-tert-butyl-4- hydroxyphenyl)propionyloxymethyl)methane and preparation thereof

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Publication number
JPS59104348A
JPS59104348A JP21305582A JP21305582A JPS59104348A JP S59104348 A JPS59104348 A JP S59104348A JP 21305582 A JP21305582 A JP 21305582A JP 21305582 A JP21305582 A JP 21305582A JP S59104348 A JPS59104348 A JP S59104348A
Authority
JP
Japan
Prior art keywords
compound
water
spherical
tetrakis
butyl
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP21305582A
Other languages
Japanese (ja)
Other versions
JPH0437820B2 (en
Inventor
Takashi Tamura
隆司 田村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP21305582A priority Critical patent/JPS59104348A/en
Publication of JPS59104348A publication Critical patent/JPS59104348A/en
Publication of JPH0437820B2 publication Critical patent/JPH0437820B2/ja
Granted legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To obtain the titled spherical or semispherical compound having a novel gamma crystal structure and a low melting point, by dropping a melt of the aimed compound onto the surface of a solid or water or extruding the melt in an inert gas or water in the form of drops, and solidifying the extruded drops. CONSTITUTION:A melt of tetrakis [3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionyloxymethyl] methane expressed by the formula is dropped onto the surface of a smooth solid, e.g. a metallic plate, or the surface of the water or extruded into an inert gas or water in the form of drops, cooled and solidified to give the aimed spherical or semispherical compound expressed by the formula having gamma crystal structure. The compound expressed by the formula is used as an antioxidant for polyolefin, etc., but powder thereof having <=100mu particle diameter is not easily handled in the aspects of automatic measurement, supply, transportation, storage, etc. However, the above-mentioned compound, expressed by the formula, and having the novel gamma crystal structure has a remarkably low melting point (60-70 deg.C lower than that of the conventional compound), and uniform dispersion by melting is easily obtained.

Description

【発明の詳細な説明】 本発明は、球状もしくは半球状であるT晶構造のテトラ
キス[:3−(3,5−ジー【−ブチル−4−ヒドロキ
シフェニル)プロピオニルオキシメチルコメタンおよび
その製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides tetrakis[:3-(3,5-di[-butyl-4-hydroxyphenyl)propionyloxymethylcomethane] having a spherical or hemispherical T crystal structure and a method for producing the same. Regarding.

下記式(I) / −C4Hg で示されるテトラキス[3−(3,5−ジ−t−ブチル
ー4−ヒドロキシフェニル)プロピオニルオキシメチル
コメタンはポリオレフィン、ポリ塩化ビニル、ポリエス
テル、ポリスチレン、AB S樹刀旨、ポリウレタン、
ポリアセタール、植物油、鉱物油などの酸化防止剤とし
て広く用いられているが、該化合物は一般に粒子径10
0μ以下の粉末状で市販されているため、飛散し易く、
流動性に乏しく、微粉による作業環境を悪化させたシ、
輸送および貯蔵中にブロック化して計量供給性を聞書す
るなどの諸欠点を有している。また、化合物(1)の実
用面で加工温度が制限される熱可塑性材料例えばポリ塩
化ビニル、ポリプロピレンあるいはアクリロニトリルー
プクジエン共重合体等に対して用いられる場合、溶融し
て容易にしかも均一に混合し易い低融解点のものが要望
される。
Tetrakis[3-(3,5-di-t-butyl-4-hydroxyphenyl)propionyloxymethylcomethane represented by the following formula (I) / -C4Hg] is a polyolefin, polyvinyl chloride, polyester, polystyrene, ABS resin. effect, polyurethane,
It is widely used as an antioxidant for polyacetal, vegetable oil, mineral oil, etc., but the compound generally has a particle size of 10
It is commercially available in powder form with a size of 0 μ or less, so it easily scatters.
Poor fluidity and poor working environment due to fine powder.
It has various drawbacks, such as being blocked during transportation and storage, which makes it difficult to measure and supply. In addition, when compound (1) is used for thermoplastic materials whose processing temperature is limited for practical reasons, such as polyvinyl chloride, polypropylene, or acrylonitrile-cyclodiene copolymer, it can be melted and mixed easily and uniformly. A material with a low melting point that is easy to melt is desired.

本発明の目的は前記の諸欠点を改善して自動計量、供給
性、輸送、貯蔵性および取扱い作業性を容易ならしめる
ために化合物(1)を最も理想的形態である球状ないし
は半球状化すると共に実用上より均一混合の容易な低融
解点化をはかり、従来迄には見出せなかった形態と低融
点である化合物(1)を提供しようとしたものである。
The purpose of the present invention is to form the compound (1) into a spherical or hemispherical form, which is the most ideal form, in order to improve the above-mentioned drawbacks and facilitate automatic measurement, supplyability, transportation, storage, and handling workability. At the same time, the aim is to lower the melting point so that it can be mixed more uniformly than in practical use, and to provide a compound (1) that has a form and a low melting point that have not been found heretofore.

従来、化合物(1)を製品化する方法としては例えば3
−(3,5−ジー【−ブチル−4−ヒドロキシフェニル
)プロピオン酸メチル(a)とペンタエリスリトール(
blとの反応生成物の熱へブタン溶液を冷却し、生成す
る固形物を沖過し、該固形物を冷ヘキサンで洗浄乾燥す
る方法−(・特公昭42−18617 )、95チイツ
プロバノールて精製した後、ヘプタンで再結晶し、水洗
乾燥する方法(特公昭42−19083 )、前記反応
生成物とエタノールで再結晶する方法(特公昭49−9
464.4 )等の方法があり、また特開昭56−12
341には化合物(1)を含む飴状物質をインブタノー
ルにより再結晶させる方法がそれぞれ開示されている。
Conventionally, methods for commercializing compound (1) include, for example, 3
-(3,5-di[-butyl-4-hydroxyphenyl)methyl propionate (a) and pentaerythritol (
A method of cooling a hot butane solution of the reaction product with bl, filtering the resulting solid, and washing and drying the solid with cold hexane - (Japanese Patent Publication No. 18617/1973), 95 Chitsu Probanol A method of recrystallizing with heptane, washing and drying with water (Japanese Patent Publication No. 42-19083), and a method of recrystallizing the reaction product with ethanol (Japanese Patent Publication No. 49-1983)
There are methods such as
No. 341 discloses a method of recrystallizing a candy-like substance containing compound (1) using inbutanol.

しかしながらこれらは何れも再結晶法によって単に白色
微結晶が得られるという方法であって、化合物f1+を
実用するまでの好ましい形態品を得るための技術に関し
ては示されていない。
However, in all of these methods, white microcrystals are simply obtained by a recrystallization method, and no technique for obtaining a desirable form of compound f1+ for practical use is disclosed.

一方、化合物(1)を良好な形態ならしめる方法として
は前記した原料(a)および(b)の反応を下記一般式
で示される化合物(2) の存在下でイー1ない、こメに得られる生成物と分子付
加体を形成する性質のあるアルコール類を添加して分子
付加体となし、更にメタノールまたは/およびエタノー
ルにょシ再結晶して流、れ性の良好な細粒として取得す
る方法(特開昭56−99444、特開昭56−139
438 )がある。
On the other hand, as a method for forming compound (1) into a good form, the above-mentioned raw materials (a) and (b) are reacted in the presence of compound (2) represented by the following general formula. A method of forming a molecular adduct by adding an alcohol having the property of forming a molecular adduct with the product, and then recrystallizing it in methanol or/and ethanol to obtain fine particles with good flowability. (JP-A-56-99444, JP-A-56-139
438).

しかし、か\る方法では最終製品化のために高価でかつ
取扱い上危険な存機溶剤を多量に必要とし精製操作自体
も極めて煩雑であシ、また得られる製品の融解点も高く
、求められる業界ニーズを十分滴定させるには至ってい
ない。また後者の文献には低融解点のT晶形品について
の記述もみられるが、ガラス状であって粉砕工程が必要
であると記載しているに過ぎない。
However, such a method requires a large amount of expensive and dangerous solvent to handle, the purification process itself is extremely complicated, and the resulting product has a high melting point, which is required. It has not yet been fully titrated to meet industry needs. The latter document also describes a T-crystal product with a low melting point, but it merely states that it is glass-like and requires a pulverization process.

本発明者はか\る事情に鑑み、化合物(1)を球状ない
しは半球状化すると共に低融解点を有するT構造のもの
として容易に取得し得る方法について鋭意研究した結果
、溶融状態の化合物(1)を平滑な固体表面上例えば金
属板等の表面上または水面上あるいは空気、窒素等の不
活性気体ソ・ 中に滴下して冷却固化させる方法が有効であjlしかも
市販される化合物(1)よシも融点が60〜70℃低い
T構造の化合物(1)として容易に亮収率で得ることが
できることを見出し本発明を完成するに至った。
In view of the above circumstances, the present inventor conducted intensive research on a method of making compound (1) spherical or hemispherical and easily obtaining it as a T-structure having a low melting point. It is effective to drop 1) onto a smooth solid surface, such as a metal plate, on a water surface, or into an inert gas such as air or nitrogen, and cool and solidify it. ) It was discovered that the compound (1) having a T structure having a melting point 60 to 70° C. lower can be easily obtained in a good yield, leading to the completion of the present invention.

前記式(1)で示されるT構造であって、かつ球状ない
し半球状液は本発明者によって初めて製造することがで
きたものであって次のような方法によって製造すること
ができる。
The liquid having the T structure represented by the above formula (1) and having a spherical or hemispherical shape was first produced by the present inventor, and can be produced by the following method.

(A)  化合物(1)の溶融物を平滑な固体表面上に
滴下し、該表面上で冷却、固化させる方法。
(A) A method in which a melt of compound (1) is dropped onto a smooth solid surface, and is cooled and solidified on the surface.

凹 化合物(1)の溶融物を水面上に滴下するか水中に
滴状に吐出し、水中で冷却、固化させる方法。
Concave A method in which the molten compound (1) is dropped onto the water surface or discharged dropwise into the water, and then cooled and solidified in the water.

(C)  化合物(1)の溶融物を不活性気体中に滴状
に吐出し、該気体中で冷却、固化させる方法。
(C) A method in which the melted compound (1) is discharged dropwise into an inert gas, and is cooled and solidified in the gas.

以下、上記諸方法について具体的に説明する。The above methods will be explained in detail below.

四の方法において、平滑な固体表面を形成するための材
質としてはその表面が平滑にな9得るものであれは特に
制限なく用いられ、たとえばアルミニウム、銅、鉄、ス
テンレスなどの金属板、シリコンなどの離型剤を塗布し
てその表面の剥離性を改良した板紙などの紙状構造物、
スチロール、テフロン、ポリプロピレンなどのプラスチ
ック板などが例示されるが、熱伝導性が良好で、化合物
(1)の溶融物を滴下した場合の冷却効果および冷却固
化物の固体表面からの剥離性などの点で特に金属板が好
ましく、と9わけアルミニウム板、アルマイト表面加工
のアルミニウム板およびステンレス板が好ましい。
In method 4, any material that can be used to form a smooth solid surface can be used without any particular restriction as long as the surface can be made smooth, such as metal plates such as aluminum, copper, iron, and stainless steel, silicon, etc. paper-like structures, such as paperboard, coated with a release agent to improve the releasability of its surface;
Plastic plates such as styrene, Teflon, and polypropylene are exemplified, but they have good thermal conductivity, have a cooling effect when the molten compound (1) is dropped, and have a good releasability of the cooled solidified material from the solid surface. In this respect, a metal plate is particularly preferred, and an aluminum plate, an aluminum plate with an alumite surface treatment, and a stainless steel plate are particularly preferred.

もちろん、これら固体の表面は冷却固化物が容易に剥離
し得るように平滑(こしておく必要がある。
Of course, the surfaces of these solids need to be smooth so that the cooled and solidified material can be easily peeled off.

この方法を実施するにあたっては、固体表面(固体板)
上から所定の距離をおいて設けたノズルから化合物(1
)の溶融物を一定量づつ滴下し、滴下物を固体表面上で
冷却して固化させ、次いでこれを固体表面から剥離、捕
集すればよい。
In implementing this method, a solid surface (solid plate)
A compound (1
) is dropped in a fixed amount at a time, the dropped material is cooled and solidified on the solid surface, and then it is peeled off from the solid surface and collected.

この際、ノズルまたは同体表面のいずれか一方を走行式
にし、他方を固定させる方法が実用上好ましく、特に走
行しつつある固体板上に化合物(1)の溶融物を滴下さ
せる方法が好ましい。
In this case, it is practically preferable to make either the nozzle or the surface of the same body mobile while the other is fixed, and particularly preferable is a method in which the melt of compound (1) is dripped onto a moving solid plate.

溶融状の化合物(1)を受ける固体表面の温度は通常5
〜40℃、好ましくは10〜30℃である。
The temperature of the solid surface that receives the molten compound (1) is usually 5
-40°C, preferably 10-30°C.

溶融物の滴下に伴って固体表面の温度上昇がみられる場
合には、任意の位置、任意の方法で所定温度を維持する
ように冷却することが必要であシ、たとえば固体表面へ
の冷風のブロー等の方法が採用される。このi合、固体
表面での結露を避けるため、その雰囲気における露点以
上の温度であることが好ましい。
If the temperature of the solid surface increases as the melt drips, it is necessary to cool it at any location and by any method to maintain the specified temperature. For example, by blowing cold air onto the solid surface. A method such as blowing is employed. In this case, in order to avoid dew condensation on the solid surface, the temperature is preferably higher than the dew point of the atmosphere.

所定の位置に設けたノズルから水面上に滴下する方法と
、水中に設けたノズルから滴状に水中に吐出する方法が
あるが、両手段は単に滴下方法が異るのみともいうべく
、本質的な相違はない。水温が5℃以下では得られる製
品が脆化し易く、また25℃よシ高温では固化速度が遅
くなり、製品の形状が偏平となり易い。また界面活性剤
の少量を溶解させておけば該溶融物の冷却同化過程で固
化物の分散が容易となシ、疎化温度で4 Q dyne
以下になるような界面活性剤であれはよく、なお低温性
のものが好ましく用いられ、具体的にはノニオン系活性
剤例えはエマルゲンpp −150(花王アトラス社品
)が水溶液の濃度で0005〜0゜2重量係となるよう
に用いられる。
There are two methods: one method is to drop drops onto the water surface from a nozzle installed at a predetermined position, and the other method is to discharge droplets into the water from a nozzle installed underwater, but the two methods are simply different in the method of dropping. There is no difference. If the water temperature is below 5°C, the resulting product will easily become brittle, and if the water temperature is higher than 25°C, the solidification rate will be slow and the product will tend to have a flat shape. In addition, if a small amount of surfactant is dissolved, it will be easier to disperse the solidified material during the cooling and assimilation process of the molten material.
Any surfactant having the following properties may be used, and a low-temperature one is preferably used. Specifically, a nonionic surfactant such as Emulgen pp-150 (Kao Atlas Co., Ltd.) has an aqueous solution concentration of 0005 to 0005. It is used so that the weight ratio is 0°2.

なお該溶融物の水面への滴下中または水中に滴状に吐出
中は水面が常時移動するように水面が波立たない程度で
適夏な流れを保つことが望ましい。
Note that while the melt is being dropped onto the water surface or being discharged dropwise into the water, it is desirable to maintain a suitable flow so that the water surface does not ripple so that the water surface is constantly moving.

水中で冷却、固化された固化物は球状ないしは半球状で
あシ、水よシ分離し乾燥して最終製品とする。
The solidified product cooled and solidified in water is spherical or hemispherical, separated from the water, and dried to form the final product.

化合物(1)の溶融物を不活性気体中に滴状に吐出落下
し、冷却固化させる方法(C)において不活性気体とし
ては空気または窒素等であるが、通常は空気が用いられ
る。すなわち、該溶融物を塔内の気流中に所定の高さに
保持されたノズルから滴状に落下させ、該塔内底部に到
達するまでの過程で冷却固化させる。この場合の気体の
温度は前記(Alの方法における固体表面の温度と同じ
である。かくして得られる製品は球状ないし半球状であ
シこれを捕集すれはよい。
In the method (C) in which the molten compound (1) is discharged dropwise into an inert gas and cooled and solidified, the inert gas is air, nitrogen, etc., and usually air is used. That is, the molten material is dropped dropwise from a nozzle held at a predetermined height into the airflow inside the tower, and is cooled and solidified in the process until it reaches the bottom of the tower. The temperature of the gas in this case is the same as the temperature of the solid surface in the above-mentioned (Al method).The product thus obtained has a spherical or hemispherical shape, and it is easy to collect it.

方法fc)で用いられる塔の高さは5〜2’Orn、通
常は10〜20mであシ、塔の筒さが十分な場合は該落
下物を平板な皿型槽で受取めればよいが、塔高が不十分
な場合は該落下物の冷却が不十分となるため10〜30
’Cの水を入れた槽に受取めるのが好ましい。なおこの
場合、受取い。
The height of the tower used in method fc) is 5 to 2' or, usually 10 to 20 m, and if the tower is sufficiently cylindrical, it is sufficient to receive the fallen material in a flat plate-shaped tank. However, if the height of the tower is insufficient, the cooling of the fallen objects will be insufficient, so the
It is preferable to receive it in a tank containing water of 'C. In this case, the receipt.

前記(Al、(B)および(C1の何れの方法において
も得られる製品の直径は滴下または滴状に吐出させる場
合に用いるノズルの口径と形状および滴下または吐出圧
力により調節されるが、通常はかくして得られる製品の
直径0゜1〜10 mm 、好ましくは0.3〜4謔で
ある。
The diameter of the product obtained in any of the above methods (Al, (B) and (C1) is adjusted by the diameter and shape of the nozzle used for dropping or discharging in droplets, and the dropping or discharging pressure, but usually The diameter of the product thus obtained is 0.1 to 10 mm, preferably 0.3 to 4 mm.

かくして得られる本発明製品の融解点を示差熱分析計に
ょシ測定した結果、49℃を示し、従来市販の化合物(
1)が同様な測定では110〜119℃の範囲にあるも
のに比ベロ0P−70’C低下しておシ、また、該製品
の結晶構造をX線回折スペクトルにょ9粉末法で測定し
たところ市販化合物(1)ではα晶またはβ晶あるいは
αとβの混合晶であるのに対してT晶であることが確認
された。
As a result of measuring the melting point of the thus obtained product of the present invention using a differential thermal analyzer, it was found to be 49°C, which is higher than that of conventional commercially available compounds (
1) was found to be lower than that in the range of 110 to 119°C in the same measurement, and the crystal structure of the product was measured by the X-ray diffraction spectrum using the 9 powder method. It was confirmed that the commercially available compound (1) was an α crystal, a β crystal, or a mixed crystal of α and β, whereas it was a T crystal.

また本発明で得られる製品は嵩比重の測定では0゜6に
9/lの値を示し極めて優れた粒状体であることと共に
硬さも適当であυ例えば直径2.5 mmの場合で50
0 y〜800 Fの硬さを有するものである。
In addition, the bulk specific gravity of the product obtained by the present invention was measured to be 9/l at 0°6, indicating that it is an extremely excellent granular material and has appropriate hardness, e.g.
It has a hardness of 0 y to 800 F.

不発明によるT構造であって球状ないし半球状である化
合物(1)なる製品は従来問題であった自動計量、供給
、輸送、貯蔵および取扱い上の該欠点を解消し更に融解
点が著るしく低いといという特徴をも有し、低融点また
は低軟化点の対象物に対してもその中に均一に分散させ
るためのロールあるいはバンバリーミキサ−等の混合装
置の温度を大巾に低下させることができる。
The uninvented compound (1), which has a T structure and is spherical or hemispherical, solves the conventional problems in automatic weighing, supply, transportation, storage, and handling, and also has a remarkable melting point. It also has the feature of low temperature, and can significantly lower the temperature of mixing equipment such as rolls or Banbury mixers to uniformly disperse objects with low melting points or low softening points. can.

特に混合時に温度が制限されるポリ塩化ビニル、ポリプ
ロピレンあるいはアクリロニトリル−ブタジェン共重合
体等への応用の際、溶融による均一分散が容易に得られ
る。
Particularly when applied to polyvinyl chloride, polypropylene, or acrylonitrile-butadiene copolymer, etc., where temperature is restricted during mixing, uniform dispersion by melting can be easily obtained.

また、植物油、鉱物油への応用では現行市販品は予め適
当な溶剤を用いてm製された溶液を添加する必要があり
、また混合に高温加熱を要し、それらの油の劣化を招く
こともあったが、本発明製品は低温で溶融するため均一
分散、が容易である。とシわけ混合温度が制限されるコ
ーン油、椿油、スピンドル油等に好ましく用いることが
できる。
In addition, when applied to vegetable oils and mineral oils, current commercially available products require the addition of a solution prepared in advance using an appropriate solvent, and high temperature heating is required for mixing, which can lead to deterioration of the oil. However, since the product of the present invention melts at a low temperature, it is easy to uniformly disperse it. It can be preferably used for corn oil, camellia oil, spindle oil, etc. where the mixing temperature is limited.

以下、本発明を実施例によって説明する。Hereinafter, the present invention will be explained by examples.

実施例 融点113℃、β晶である市販の化合物(1)を加熱溶
融し、145〜160℃で窒素ガス雰囲気中に保持し、
多数の滴下ノズル(内径2mm)を付けた定量滴下注入
装置から一定量づつ移動する20℃のアルミニウム板(
表面はアルマイト加工であシ裏面は水で濡らした布と接
4aさせて除熱した)上に滴下したところ15秒で固化
し、該板上で冷却固化した製品を捕集した。こ\に得ら
れた製品は直径2〜3 mmの透明な球状であ多、示差
熱分析による吸熱ピークが49℃で最大に達する融解点
を有し、X線回折によ)T構造を示し、また嵩比重0゜
6即/l、硬度600ノ荷重、安息角30°であり、実
用上十分な硬さと流れ性を有する粒子であった。
Example A commercially available compound (1) having a melting point of 113°C and a β-crystal is melted by heating and held in a nitrogen gas atmosphere at 145 to 160°C,
A 20°C aluminum plate (
The surface was alumite-treated and the back surface was removed by contacting it with a cloth moistened with water (4a) to remove heat), and it solidified in 15 seconds, and the solidified product was collected by cooling on the plate. The product thus obtained is transparent and spherical with a diameter of 2 to 3 mm, has a melting point with an endothermic peak reaching its maximum at 49°C according to differential thermal analysis, and exhibits a T structure according to X-ray diffraction. In addition, the particles had a bulk specific gravity of 0°6/l, a hardness under a load of 600, and an angle of repose of 30°, and had sufficient hardness and flowability for practical use.

実施例2 融点113〜120℃、αとβの混合晶である市販の化
合物(1)を加熱溶融し、155〜165℃で窒素ガス
雰囲気中圧力0゜5Kti/crh2に保持し多数の滴
下ノズル(内径1.)を付けた定量注入装置から高さ1
0%の20℃の空気を通じた塔内に重下させたが、僅か
5秒間で固化した。かくして得られた製品は直径0゜5
〜1゜2mmの球状であシ、示差熱分析による融点は4
9℃、またX線回折によpr構造を示し、嵩比重0.6
2KP/l!、安息角28°の実用上十分な硬さと流れ
性の優れた粒子であった。
Example 2 A commercially available compound (1) having a melting point of 113 to 120°C and a mixed crystal of α and β was melted by heating, and the mixture was maintained at a pressure of 0°5 Kti/crh2 in a nitrogen gas atmosphere at 155 to 165°C, and then passed through a number of dropping nozzles. Height 1 from metered injection device with (inner diameter 1.)
The mixture was placed in a tower through which 0% air at 20°C was passed, but it solidified in just 5 seconds. The product thus obtained has a diameter of 0°5.
~1°2mm spherical shape, melting point according to differential thermal analysis is 4
9℃, and X-ray diffraction shows pr structure, bulk specific gravity 0.6
2KP/l! The particles had a repose angle of 28°, sufficient hardness for practical use, and excellent flowability.

実施例3 融点120℃、α晶である市販化合物(1)を加熱溶融
し、150〜160℃で窒素ガス雰囲気中に保持し、多
数の滴下ノズル(内径2〜b■)を付けた定量注入装置
から一定量づつ、深さを 速度で流れを支えたものである。滴下後5秒間で固化し
固化物は流水中で沈降した。これを捕集して水を切シ、
風乾して直径2〜4 rrLwnの球状製品を得た。か
くして得られた製品は実施例1と同様な測定により、融
点49℃、T構造を示し嵩比重0662即/l、硬度5
00ノ荷重、安息角30°の実用上十分な硬さと優れた
流れ性を有する粒子であった。
Example 3 A commercially available compound (1) with a melting point of 120°C and α crystal was melted by heating, maintained at 150 to 160°C in a nitrogen gas atmosphere, and quantitatively injected using a large number of dropping nozzles (inner diameter 2 to b■). The flow is supported by a fixed amount from the device at a certain depth and speed. It solidified within 5 seconds after dropping, and the solidified material settled in running water. Collect this and drain the water.
After air drying, a spherical product with a diameter of 2-4 rrLwn was obtained. The thus obtained product was measured in the same manner as in Example 1, and was found to have a melting point of 49°C, a T structure, a bulk specific gravity of 0662 mm/l, and a hardness of 5.
The particles had practically sufficient hardness with a load of 0.00 and an angle of repose of 30° and excellent flowability.

実施例4 実施例3と同様な装置および操作によシ同と じ市販化合物(1)の溶融物l界面活性剤エマルゲン9
05(花王アトラス社品、ノニオン系)0゜1重量%を
溶解した20℃の流水面上に滴下したところ5秒間で固
化した。かくして得られた製品は球状を呈し、直径2〜
4 mmのものであり、融点49℃、T構造を示し実用
上十分な硬度と優れた流れ性を有するものであった。
Example 4 Using the same apparatus and operation as in Example 3, a melt of the same commercially available compound (1) l surfactant Emulgen 9 was prepared.
05 (manufactured by Kao Atlas Co., Ltd., nonionic type) When dropped onto the surface of running water at 20°C in which 0.1% by weight had been dissolved, it solidified in 5 seconds. The product thus obtained has a spherical shape, with a diameter of 2~
It was 4 mm thick, had a melting point of 49° C., had a T structure, had sufficient hardness for practical use, and had excellent flowability.

実施例5 実施例1と同様な装置および操作により同じ市販化合物
(1)の溶融物を移動する20 ℃のシリコン離型紙表
面上に滴下したところ、30秒間で固化した。こ\に得
られた製品は直径2〜3 mm  の半球状であシ、融
点49℃、T構造を示し、かつ、実用上十分な硬度と優
れた流れ性を有するものであった。
Example 5 Using the same equipment and operation as in Example 1, a melt of the same commercially available compound (1) was dropped onto the surface of a moving silicon release paper at 20°C, and it solidified in 30 seconds. The product thus obtained had a hemispherical shape with a diameter of 2 to 3 mm, a melting point of 49° C., a T structure, and sufficient hardness for practical use and excellent flowability.

手続補正書(自発)6゜ (1) 昭和58年 1月ノダ日 1 中外の表示 昭和57年 特許願第213055  号2 発明の名
称 球状もしくは半球状のテトラキス[−(3,5−シーt
−アーチルー1−4−ヒドロキシフェニル)フロピオニ
ルオキシメチル〕メタンおよびその製造方法3 補正を
才る名 ・Jl’lとの関係   特許出願人 渕 7゜ := 住 所  大阪市東区北浜5丁目15番地つ 明細書の発明の詳細な説明の欄 補正の内容 明細書第10頁第5行目に[−低温性−1とあるを「低
起泡性」と補正する。
Procedural amendment (spontaneous) 6゜(1) January 1, 1981 Chugai Indication 1982 Patent Application No. 213055 2 Name of the invention Spherical or hemispherical tetrakis [-(3,5-sheet
-Archilu 1-4-hydroxyphenyl)flopionyloxymethyl]methane and its manufacturing method 3 Relationship with Jl'l name subject to amendment Patent applicant Fuchi7゜:= Address 5-15 Kitahama, Higashi-ku, Osaka Address: Contents of amendment in the Detailed Description of the Invention column of the specification In the 5th line of page 10 of the specification, [-Low-temperature property-1] is corrected to read 'low foaming property'.

以  上that's all

Claims (5)

【特許請求の範囲】[Claims] (1)  球状もしくは半球状であるγ晶構造のテトラ
キス[:3−(3,5−ジ−t−ブチル−4−ヒドロキ
シフェニル)プロピオニルオキシメチルコメタン。
(1) Tetrakis[:3-(3,5-di-t-butyl-4-hydroxyphenyl)propionyloxymethylcomethane] having a spherical or hemispherical gamma crystal structure.
(2)  テトラキス[3−(3,5−ジ−t−ブチル
−4−4:)’ロキシフェニル)フロピオニルオキシメ
チルコメタンの溶融物を平滑な固体表面上に滴下し、冷
却固化させることを特徴とする球状もしくは半球状であ
るγ晶構造のテトラキス[3−(3,5−ジーに一ブチ
ルー4−ヒドロキシフェニル)プロピオニルオキシメチ
ルコメタンの製造方法。
(2) Drop the melt of tetrakis[3-(3,5-di-t-butyl-4-4:)'roxyphenyl)propionyloxymethylcomethane onto a smooth solid surface and solidify by cooling. A method for producing tetrakis[3-(3,5-di-butyl-4-hydroxyphenyl)propionyloxymethylcomethane] having a spherical or hemispherical gamma crystal structure, characterized by the following.
(3)平滑な固体表面が金属板表面である特許請求の範
囲第2項に記載の製造方法。
(3) The manufacturing method according to claim 2, wherein the smooth solid surface is a metal plate surface.
(4)  テトラキス[3−(3,5〜ジー【−ブチル
−4−ヒドロキシフェニル)フロピオニルオキシメチル
コメタンの溶融物を不活性気体中に滴状に吐出、冷却、
固化させることを特徴とする球状もしくは半球状である
γ晶構造のテトラキス[:3−(3,5−ジー【−ブチ
ル−4−ヒドロキシフェニル)プロピオニルオキシメチ
ルコメタンの製造方法。
(4) Dispense the melt of tetrakis[3-(3,5-di[-butyl-4-hydroxyphenyl)propionyloxymethylcomethane] dropwise into an inert gas, cool it,
A method for producing tetrakis[:3-(3,5-di[-butyl-4-hydroxyphenyl)propionyloxymethylcomethane] having a spherical or hemispherical γ-crystal structure, which is characterized by solidifying.
(5)  テトラキス(3−(3,5−ジ−t−ブチル
−4−k= トロキシフェニル)フロピオニルオキシメ
チルコメタンの溶融物を水面上に滴下するかまたは水中
に滴状に吐出して、水中で冷却固化させることを特徴と
する球状もしくは半球状であるγ晶構造のテトラキス〔
3−(3,5−ジー(−ブチル−4−ヒドロキシフェニ
ル)プロピオニルオキシメチルコメタンの製造方法。
(5) Drop the melt of tetrakis(3-(3,5-di-t-butyl-4-k=troxyphenyl)propionyloxymethylcomethane) onto the water surface or discharge it dropwise into the water. Tetrakis [
A method for producing 3-(3,5-di(-butyl-4-hydroxyphenyl)propionyloxymethylcomethane).
JP21305582A 1982-12-03 1982-12-03 Spherical or semispherical tetrakis (3-(3,5-di-tert-butyl-4- hydroxyphenyl)propionyloxymethyl)methane and preparation thereof Granted JPS59104348A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21305582A JPS59104348A (en) 1982-12-03 1982-12-03 Spherical or semispherical tetrakis (3-(3,5-di-tert-butyl-4- hydroxyphenyl)propionyloxymethyl)methane and preparation thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21305582A JPS59104348A (en) 1982-12-03 1982-12-03 Spherical or semispherical tetrakis (3-(3,5-di-tert-butyl-4- hydroxyphenyl)propionyloxymethyl)methane and preparation thereof

Publications (2)

Publication Number Publication Date
JPS59104348A true JPS59104348A (en) 1984-06-16
JPH0437820B2 JPH0437820B2 (en) 1992-06-22

Family

ID=16632779

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPS59104348A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0210131A2 (en) * 1985-07-19 1987-01-28 Ciba-Geigy Ag Solvent-free crystallization of pentaerythritol tetrakis-[-3-(3,5-di-tert. butyl-4-hydroxyphenyl)-propionate] and its lambda crystalline form
EP0244361A2 (en) * 1986-04-30 1987-11-04 Ciba-Geigy Ag Individual beta-form crystals of tetrakis-[3-(3,5-di-t-butyl-4-hydroxyphenyl)-propionyloxymethyl] methane and process for their manufacture
JPS6335544A (en) * 1986-07-25 1988-02-16 エニーケム・シンテシース・エセ・ピ・ア Amorphous tetrakis(3-(3,5-ditertiary-butyl-4- hydroxyphenyl)-propionyl-oxymethyl)methane, manufacture and stabilized polymer composition
US6225375B1 (en) 1997-04-15 2001-05-01 Ciba Specialty Chemicals Corporation Preparation of low-dust stabilizers
EP0514784B2 (en) 1991-05-17 2005-10-05 Great Lakes Chemical (Europe) GmbH Process for granulating additives for organic polymers

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56139438A (en) * 1980-04-01 1981-10-30 Mitsui Petrochem Ind Ltd Tetrakis 3- 3,5-di-t-butyl-4-hydroxyphenyl - propionyloxymethyl methane having new crystal structure

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56139438A (en) * 1980-04-01 1981-10-30 Mitsui Petrochem Ind Ltd Tetrakis 3- 3,5-di-t-butyl-4-hydroxyphenyl - propionyloxymethyl methane having new crystal structure

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0210131A2 (en) * 1985-07-19 1987-01-28 Ciba-Geigy Ag Solvent-free crystallization of pentaerythritol tetrakis-[-3-(3,5-di-tert. butyl-4-hydroxyphenyl)-propionate] and its lambda crystalline form
EP0210131A3 (en) * 1985-07-19 1987-09-09 Ciba-Geigy Ag Solvent-free crystallization of pentaerythritol tetrakis-û-3-(3,5-di-tert. butyl-4-hydroxyphenyl)-propionate¨ and its lambda crystalline form
EP0244361A2 (en) * 1986-04-30 1987-11-04 Ciba-Geigy Ag Individual beta-form crystals of tetrakis-[3-(3,5-di-t-butyl-4-hydroxyphenyl)-propionyloxymethyl] methane and process for their manufacture
JPS6335544A (en) * 1986-07-25 1988-02-16 エニーケム・シンテシース・エセ・ピ・ア Amorphous tetrakis(3-(3,5-ditertiary-butyl-4- hydroxyphenyl)-propionyl-oxymethyl)methane, manufacture and stabilized polymer composition
EP0514784B2 (en) 1991-05-17 2005-10-05 Great Lakes Chemical (Europe) GmbH Process for granulating additives for organic polymers
US6225375B1 (en) 1997-04-15 2001-05-01 Ciba Specialty Chemicals Corporation Preparation of low-dust stabilizers
US6740694B2 (en) 1997-04-15 2004-05-25 Ciba Specialty Chemicals Corporation Preparation of low-dust stabilisers

Also Published As

Publication number Publication date
JPH0437820B2 (en) 1992-06-22

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